• 专利标题:   Formation of biomass-derived hydrocarbon feedstock used for forming e.g. bio-derived liquefied petroleum gas, involves pyrolyzing low-moisture biomass feedstock to form mixture of biochar, hydrocarbon feedstock, non-condensable light gases and water, and separating hydrocarbon feedstock from mixture.
  • 专利号:   WO2022063937-A1, GB2599374-A, GB2608923-A, AU2021346852-A1
  • 发明人:   ATKINS M
  • 专利权人:   ABUNDIA BIOMASSTOLIQUIDS LTD, ABUNDIA BIOMASSTOLIQUIDS LTD
  • 国际专利分类:   C10B053/02, C10B057/10, C10B057/16, C10G003/00, C10G031/09, C10G045/08, C10G045/12, C10G045/62, C10G045/64, C10G049/04, C10G049/06, C10G049/08, C10L001/04, C10L005/44, C10L009/08, C10B053/00, C10G001/00, C10L001/00
  • 专利详细信息:   WO2022063937-A1 31 Mar 2022 202234 Pages: 50 English
  • 申请详细信息:   WO2022063937-A1 WOEP076277 23 Sep 2021
  • 优先权号:   GB014336, GB015247

▎ 摘  要

NOVELTY - Formation of a biomass-derived hydrocarbon feedstock involves ensuring the moisture content of a biomass feedstock is 10 wt.% or less, pyrolyzing the low-moisture biomass feedstock at more than 950 degrees C to form a mixture of biochar, a hydrocarbon feedstock, non-condensable light gases, such as hydrogen, carbon monoxide, carbon dioxide and methane, and water, and separating the hydrocarbon feedstock from the mixture. USE - Formation of biomass-derived hydrocarbon feedstock used for forming bio-derived liquefied petroleum gas (all claimed). Can also be used for producing jet fuel, diesel, and naphtha. ADVANTAGE - The method economically produces biomass-derived hydrocarbon feedstock. The biomass-derived hydrocarbon feedstock produces bio-derived liquefied petroleum gas with high quality. DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) formation of a bio-derived liquefied petroleum gas fuel, which involves providing the biomass-derived hydrocarbon feedstock comprising at least 0.1 wt.% of one or more 8C compounds, at least 0.5 wt.% of one or more 10C compounds, at least 5% of one or more 12C compounds, at least 5 wt.% of one or more 16C compounds, and at least 30 wt.% of at least one or more 18C compounds, processing the hydrocarbon feedstock to produce a refined bio-oil by at least partially removing sulfur containing components from the hydrocarbon feedstock, hydro-treating the hydrocarbon feedstock, and hydro-isomerizing the hydrocarbon feedstock, and separating the bio-derived liquefied petroleum gas from the refined bio-oil; (2) the desulfurized hydrocarbon feedstock, which comprises at least 0.5 wt.% of one or more 8C compounds, at least 2 wt.% of one or more 10C compounds, at least 4 wt.% of one or more 12C compounds, at least 10 wt.% of one or more 16C compounds, and at least 25 wt.% of one or more 18C compounds; (3) the hydrotreated hydrocarbon feedstock, which comprises at least 0.5 wt.% of one or more 8C compounds, at least 6 wt.% of one or more 10C compounds, at least 4 wt.% of one or more 12C compounds, at least 3 wt.% of one or more 16C compounds, and at least 30 wt.% of one or more 18C compounds; (4) the hydro-isomerized hydrocarbon feedstock, which comprises at least 0.5 wt.% of one or more 8C compounds, at least 7.5 wt.% of one or more 10C compounds, at least 4 wt.% of one or more 12C compounds, at least 7 wt.% of one or more 16C compounds, and at least 12 wt.% of one or more 18C compounds; and (5) the refined bio-oil, which comprises at least 7.5 wt.% of one or more 10C compounds, at least 4 wt.% of one or more 12C compounds, at least 7 wt.% of one or more 15C compounds, and at least 12 wt.% of one or more 18C compounds.